<HashMap><database>biostudies-literature</database><scores/><additional><submitter>Carota E</submitter><funding>Ministero dell’Istruzione, dell’Università e della Ricerca</funding><pagination>e04801</pagination><full_dataset_link>https://www.ebi.ac.uk/biostudies/studies/S-EPMC7494470</full_dataset_link><repository>biostudies-literature</repository><omics_type>Unknown</omics_type><volume>6(9)</volume><pubmed_abstract>The aqueous extraction of orange peel waste (OPW), the byproduct of the juice extraction process generated annually in massive amounts (21 Mton), yields a carbohydrate-rich liquid fraction, termed orange peel extract (OPE). Several studies highlight that the combination of glycerol, a biodiesel byproduct, with carbohydrate mixtures might boost microbial lipid production. This study performed first a shaken flask screening of 15 oleaginous yeast strains based on their growth and lipid-producing abilities on OPE- and glycerol-based media. This screening enabled the selection of &lt;i>R. toruloides&lt;/i> NRRL 1091 for the assessment of the process transfer in a stirred tank reactor (STR). This assessment relied, in particular, on either single- and double-stage feeding fed-batch (SSF-FB and DSF-FB, respectively) processes where OPE served as the primary medium and nitrogen-containing glycerol-OPE mixtures as the feeding one. The continuous supply mode at low dilution rates (0.02 and 0.01 h&lt;sup>-1&lt;/sup> for SSF-FB and DSF-FB, respectively) starting from the end of the exponential growth of the initial batch phase enabled the temporal extension of biomass and lipid production. The SSF-FB and DSF-FB processes attained high biomass and lipid volumetric productions (LVP) and ensured significant lipid accumulation on a dry cell basis (Y&lt;sub>L/X&lt;/sub>). The SSF-FB process led to LVP of 20.6 g L&lt;sup>-1&lt;/sup> after 104 h with volumetric productivity (&lt;i>r&lt;/i> &lt;sub>L&lt;/sub>) of 0.20 g L&lt;sup>-1&lt;/sup> h&lt;sup>-1&lt;/sup> and Y&lt;sub>L/X&lt;/sub> of 0.80; the DSF-FB process yielded LVP, &lt;i>r&lt;/i> &lt;sub>L&lt;/sub> and Y&lt;sub>L/X&lt;/sub> values equal to 15.92 g L&lt;sup>-1&lt;/sup>, 0.11 g L&lt;sup>-1&lt;/sup> h&lt;sup>-1&lt;/sup> and 0.65, respectively. The fatty acid profiles of lipids from both fed-batch processes were not significantly different and resembled that of &lt;i>Jatropha&lt;/i> oil, a vastly used feedstock for biodiesel production. These results suggest that OPE constitutes an excellent basis for the fed-batch production of &lt;i>R. toruloides&lt;/i> lipids, and this process might afford a further option in OPW-based biorefinery.</pubmed_abstract><journal>Heliyon</journal><pubmed_title>Mixed glycerol and orange peel-based substrate for fed-batch microbial biodiesel production.</pubmed_title><pmcid>PMC7494470</pmcid><funding_grant_id>ARS01_00985</funding_grant_id><pubmed_authors>Crognale S</pubmed_authors><pubmed_authors>Carota E</pubmed_authors><pubmed_authors>D'Annibale A</pubmed_authors><pubmed_authors>Petruccioli M</pubmed_authors></additional><is_claimable>false</is_claimable><name>Mixed glycerol and orange peel-based substrate for fed-batch microbial biodiesel production.</name><description>The aqueous extraction of orange peel waste (OPW), the byproduct of the juice extraction process generated annually in massive amounts (21 Mton), yields a carbohydrate-rich liquid fraction, termed orange peel extract (OPE). Several studies highlight that the combination of glycerol, a biodiesel byproduct, with carbohydrate mixtures might boost microbial lipid production. This study performed first a shaken flask screening of 15 oleaginous yeast strains based on their growth and lipid-producing abilities on OPE- and glycerol-based media. This screening enabled the selection of &lt;i>R. toruloides&lt;/i> NRRL 1091 for the assessment of the process transfer in a stirred tank reactor (STR). This assessment relied, in particular, on either single- and double-stage feeding fed-batch (SSF-FB and DSF-FB, respectively) processes where OPE served as the primary medium and nitrogen-containing glycerol-OPE mixtures as the feeding one. The continuous supply mode at low dilution rates (0.02 and 0.01 h&lt;sup>-1&lt;/sup> for SSF-FB and DSF-FB, respectively) starting from the end of the exponential growth of the initial batch phase enabled the temporal extension of biomass and lipid production. The SSF-FB and DSF-FB processes attained high biomass and lipid volumetric productions (LVP) and ensured significant lipid accumulation on a dry cell basis (Y&lt;sub>L/X&lt;/sub>). The SSF-FB process led to LVP of 20.6 g L&lt;sup>-1&lt;/sup> after 104 h with volumetric productivity (&lt;i>r&lt;/i> &lt;sub>L&lt;/sub>) of 0.20 g L&lt;sup>-1&lt;/sup> h&lt;sup>-1&lt;/sup> and Y&lt;sub>L/X&lt;/sub> of 0.80; the DSF-FB process yielded LVP, &lt;i>r&lt;/i> &lt;sub>L&lt;/sub> and Y&lt;sub>L/X&lt;/sub> values equal to 15.92 g L&lt;sup>-1&lt;/sup>, 0.11 g L&lt;sup>-1&lt;/sup> h&lt;sup>-1&lt;/sup> and 0.65, respectively. The fatty acid profiles of lipids from both fed-batch processes were not significantly different and resembled that of &lt;i>Jatropha&lt;/i> oil, a vastly used feedstock for biodiesel production. These results suggest that OPE constitutes an excellent basis for the fed-batch production of &lt;i>R. toruloides&lt;/i> lipids, and this process might afford a further option in OPW-based biorefinery.</description><dates><release>2020-01-01T00:00:00Z</release><publication>2020 Sep</publication><modification>2024-02-14T20:26:07.736Z</modification><creation>2020-09-30T07:03:08Z</creation></dates><accession>S-EPMC7494470</accession><cross_references><pubmed>32984573</pubmed><doi>10.1016/j.heliyon.2020.e04801</doi></cross_references></HashMap>